Low Temperature Refrigeration Thermodynamics & Basics Main

Total Page:16

File Type:pdf, Size:1020Kb

Low Temperature Refrigeration Thermodynamics & Basics Main Low temperature refrigeration Thermodynamics & Basics Dr. Alexander Alekseev Linde AG, Innovation Management Main Topics • Definitions, 1st and 2nd law of thermodynamics etc. • Cooling effects • Refrigeration processes / cycles • Helium Refrigeration 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 2 1 Thermodynamics & Basics • Cooling • Heat flows from warm to cold objects • Refrigerator 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 3 Refrigerator, Definition Qo P ??? 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 4 2 Refrigerator, 1st law Conservation of energy Qo P Qamb 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 5 Interfaces Cooling capacity Qo Waste heat [capacity] Qamb Power P Qo Qamb P 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 6 3 Refrigerator / Water pump analogy 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 7 The 1st law: P + Qo = Qamb Cooling Capacity: Qo = 100 W Cooling Temperature: To = 100 K P = 100 W Waste Heat Qamb = 200 W P = 1 W Waste Heat Qamb = 101 W Is it possible? 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 8 4 Refrigerator, Carnot equation Tamb To PMIN Qo To Qo = 100 W To = 100 K Tamb = 300 K 300 K 100 K P 100W 200 W MIN 100 K 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 9 Min. power requirements (min. power consumption) Liquid Liquid Liquid Nitrogen Hydrogen Helium (LIN) (LH2) (LHe) Cooling temperature 77.4 20.1 4.2 To, K Required cooling 100 100 100 capacity Qo, W Min. power 288 1393 7043 requirements P, W P / Qo 2.9 13.9 70.4 All numbers calculated for ambient temperature Tamb = 300 K 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 10 5 Exercise An older cooling system is available with: Cooling Capacity: Qo = 300 W Cooling Temperature: To = 4.5 K Ambient Temperature: Tamb = 293 K = ca. 20 Cels Revamp: 4.5 K 1.8 K 4.5 K – refrigerator: Pmin = 300 W (293 K - 4.5 K) / 4.5 K = 19 233 W = 19.2 kW 1.8 K – refrigerator: Pmin = 300 W (293 K - 1.8 K) / 1.8 K = 45 833 W = 45.8 kW 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 11 COP – coefficient of performance COP = What you get / What you pay for What you get: Cooling capacity Qo = 300 W What you pay for: Power consumption P = 75 kW (assumpt.) Q COP o P COP = Qo / P = 0.3 kW / 75 kW = 0.004 = 0.4 % 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 12 6 Carnot efficiency (or CF, FOM) Cooling Capacity: Qo = 300 W Power Consumption: P = 75 kW COP: 0.4% According to Carnot equation: Tamb To 293K 4.2K PMIN Qo 0.3kW 19.2kW To 4.2K COPMAX Qo / PMIN 0.3kW /19.2kW 0.0156 1.6% Efficiency: e COP /COPMAX e 0.4% /1.6% 0.25 25% 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 13 COOLING EFFECTS • Joule-Thomson expansion • Expansion in turbine • Mixing of different fluids • Simon cooling • Peltier cooling • Vortex tube • etc. 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 14 7 Joule Thomson Expansion (adiabatic & isenthalpic) FlaschenventilValve Joule Thomson Effect: T 2 T T 2 T1 Temperature measurementTemperatur- 200200 bar bar meßgerät StickstoffN2 Joule-Thomson Coefficient: Ambient temperature: 300 K T Umgebungstemperatur:Ambient pressure: 1 bar T = 300 K = 27 C 1 p h const Umgebungsdruck: 1 bar 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 15 Joule Thomson expansion (adiabatic & isenthalpic) temperature - entropy diagram 11 1-2 H1 = H2 T 22 H3 = H4 3 , K , 3 3-4 T Temperature 44 17/04/2013 Fu17/04/2013ßzeile Low temperature refrigeration, Thermodynamics & BasicsSpecific entropy 16 sec 8 Joule Thomson Expansion, temperature - enthalpy diagram 1 300 NitrogenT,h - Diagramm, N2 280 300 bar 200 bar 2 260 100 bar 50 bar 240 40 bar 220 3 200 30 bar , K , 180 20 bar 10 bar 160 5 bar 1 bar Temperatur, K Temperatur, 140 120 Temperature 4 100 80 60 40 7000 9000 11000 13000 15000 17000 19000 21000 Specificspezifischeenthalpy Enthalpie,, J/mol J/mol 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 17 TURBINE 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 18 9 Expansion in a turbine 1st law: P = H1 – H2 P = 0 H1 = H2 (JT throttling) P > 0 H2 < H1 T2 < T1 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 19 Expansion in a turbine 1 300 NitrogenT,h - Diagramm, N2 280 300 bar 200 bar 260 100 bar 50 bar 240 40 bar 220 3 200 30 bar 20 bar , K , 180 10 bar 160 5 bar 2 1 bar Temperatur, K Temperatur, 140 120 Temperature 4 100 80 60 40 7000 9000 11000 13000 15000 17000 19000 21000 Specificspezifischeenthalpy Enthalpie,, J/mol J/mol 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 20 10 Expansion in a turbine, T,s-Diagramm 1 1 1-2 T D 3 3 , K , 3-4 T D 2 2 Temperature 4 1 4 p in Pideal M R Tin 1 1 pout Specific entropy 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 21 REFRIGERATION PROCESSES • Joule-Thomson - process / refrigerator • Brayton - process / refrigerator • Claude - process / refrigerator 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 22 11 Joule Heat exchanger Components: Hardware Main - Thomson process Thomson 17/04/2013 17/04/2013 Throttle valve Low temperature refrigeration, Thermodynamics & Basics & Thermodynamics refrigeration, Low temperature Basics & Thermodynamics refrigeration, Low temperature Heat exchanger Multi stage compressor Q o = H = 5 – H 1 23 24 12 Main Hardware Components: Heat Exchanger (Alu Plate Fin Heat Exchanger) Dimensions per core: up to 1.5 x 1.5 x 8.0 m Standard design temperature: -269 to +65°C (150°F) Design pressures: up to 115 bar (1640 psig) 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 25 Main Elements – Heat Exchanger Modular design allows scale up to any size 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 26 13 Main Hardware Components: Spiral Wound Heat Exchanger 17/04/2013 Fu17/04/2013ßzeile Low temperature refrigeration, Thermodynamics & Basics 27 JT - process: cool - down procedure 1 amb P 5 1 5 2b 3a 2c 3b 2 4 3 2d Heat , K , o 3c Cooling 2 object Temperature 3d 4 3 17/04/2013 Fu17/04/2013ßzeile Low temperature refrigeration, ThermodynamicsSpecific & Basics entropy 28 14 Liquefier / Refrigerator 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 29 JT- refrigerator Advantages: • Simple amb P • No moving parts in cold box reliable 1 • Produce liquid 5 Disadvantages: • High pressure compressor (100-200 bar) • Oil-free compressor [or with oil removal unit] • Relative high cost 2 4 • Relative high maintenance • Low efficiency 3 • Small-scale systems only Heat o • Cooling Temperatures above 70 K only, (theoretically above 50 K only) Cooling object 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 30 15 Open cycle JT- cooler (MMR Technologies) 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 31 Mixed gas JT-cooler based on an oil-lubricated compressor 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 32 16 Brayton-process Qo = Ptur + H5 – H1 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 33 Brayton-Verfahren 1. Cooling capacity Qo depends on - enthalpy difference at the warm end of heat exchanger (JT effect) - and expander [turbine] power: Qo = (H5 - H1) + Ptur 2. Working pressures used in a Brayton cycle are < 20 bar. The enthalpy difference (H5-H1) is therefore relative small: (H5 - H1) 0 3. Therefore the cooling capacity of the Brayton cycle is defined by the power of expander [turbine]: Qo ≈ Ptur 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 34 17 Brayton, T,s – Diagram, Nitrogen 11 5 , K , 2 Temperature 4 3 17/04/2013 Fu17/04/2013ßzeile Low temperature refrigeration, ThermodynamicsSpecific & Basics entropy 35 T,s-Diagram, Helium 10 bar 1 bar 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 36 18 T,s – Diagram, Helium 10 bar 2 4 1 bar 3 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 37 Brayton- refrigerator Advantages: • High efficiency • Pressure relative low • Low cooling temperature Disadvantages: • Cooling temperature To = var • Liquid production: very limited • Turbine • Oilfree compressor or with oil removal unit or turbocompressor • Small cooling capacity (< 500 W) difficult to realize 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 38 19 Brayton- Cooler 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 39 Claude - process Features: • Combination of an expander (turbine or piston expander) and JT valve (throttle) • intermediate pressure level (< 60 bar for nitrogen < 20 bar for helium) • gas at the outlet of expander • liquid at the outlet of JT valve 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 40 20 N2- Claude- Process, T-s-diagram 1 5 5a 2a 4a 2 3a 3 4 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 41 Claude- process Advantages . High efficiency . Compressor pressures relative low . Liquefaction possible . Therefore stable cooling temperature . Low cooling temperatures Disadvantages . Turbine . Oil-free compressor [or with oil removal unit] . Small cooling capacity difficult to realize 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 42 21 Overview, refrigerators 17/04/2013 Low temperature refrigeration, Thermodynamics & Basics 43 Helium Refrigeration • Main applications • Helium – Claude cycles • Helium Liquefier, PFD •
Recommended publications
  • Thermodynamics of Solar Energy Conversion in to Work
    Sri Lanka Journal of Physics, Vol. 9 (2008) 47-60 Institute of Physics - Sri Lanka Research Article Thermodynamic investigation of solar energy conversion into work W.T.T. Dayanga and K.A.I.L.W. Gamalath Department of Physics, University of Colombo, Colombo 03, Sri Lanka Abstract Using a simple thermodynamic upper bound efficiency model for the conversion of solar energy into work, the best material for a converter was obtained. Modifying the existing detailed terrestrial application model of direct solar radiation to include an atmospheric transmission coefficient with cloud factors and a maximum concentration ratio, the best shape for a solar concentrator was derived. Using a Carnot engine in detailed space application model, the best shape for the mirror of a concentrator was obtained. A new conversion model was introduced for a solar chimney power plant to obtain the efficiency of the power plant and power output. 1. INTRODUCTION A system that collects and converts solar energy in to mechanical or electrical power is important from various aspects. There are two major types of solar power systems at present, one using photovoltaic cells for direct conversion of solar radiation energy in to electrical energy in combination with electrochemical storage and the other based on thermodynamic cycles. The efficiency of a solar thermal power plant is significantly higher [1] compared to the maximum efficiency of twenty percent of a solar cell. Although the initial cost of a solar thermal power plant is very high, the running cost is lower compared to the other power plants. Therefore most countries tend to build solar thermal power plants.
    [Show full text]
  • Solar Heating and Cooling & Solar Air-Conditioning Position Paper
    Task 53 New Generation Solar Cooling & Heating Systems (PV or solar thermally driven systems) Solar Heating and Cooling & Solar Air-Conditioning Position Paper November 2018 Contents Executive Summary ............................................................. 3 Introduction and Relevance ................................................ 4 Status of the Technology/Industry ...................................... 5 Technical maturity and basic successful rules for design .............. 7 Energy performance for PV and Solar thermally driven systems ... 8 Economic viability and environmental benefits .............................. 9 Market status .................................................................................... 9 Potential ............................................................................. 10 Technical potential ......................................................................... 10 Costs and economics ..................................................................... 11 Market opportunities ...................................................................... 12 Current Barriers ................................................................. 12 Actions Needed .................................................................. 13 This document was prepared by Daniel Neyer1,2 and Daniel Mugnier3 with support by Alexander Thür2, Roberto Fedrizzi4 and Pedro G. Vicente Quiles5. 1 daniel neyer brainworks, Oberradin 50, 6700 Bludenz, Austria 2 University of Innsbruck, Technikerstr. 13, 6020 Innsbruck, Austria
    [Show full text]
  • Ammonia As a Refrigerant
    1791 Tullie Circle, NE. Atlanta, Georgia 30329-2305, USA www.ashrae.org ASHRAE Position Document on Ammonia as a Refrigerant Approved by ASHRAE Board of Directors February 1, 2017 Expires February 1, 2020 ASHRAE S H A P I N G T O M O R R O W ’ S B U I L T E N V I R O N M E N T T O D A Y © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. COMMITTEE ROSTER The ASHRAE Position Document on “Ammonia as a Refrigerant” was developed by the Society’s Refrigeration Committee. Position Document Committee formed on January 8, 2016 with Dave Rule as its chair. Dave Rule, Chair Georgi Kazachki IIAR Dayton Phoenix Group Alexandria, VA, USA Dayton, OH, USA Ray Cole Richard Royal Axiom Engineers, Inc. Walmart Monterey, CA, USA Bentonville, Arkansas, USA Dan Dettmers Greg Scrivener IRC, University of Wisconsin Cold Dynamics Madison, WI, USA Meadow Lake, SK, Canada Derek Hamilton Azane Inc. San Francisco, CA, USA Other contributors: M. Kent Anderson Caleb Nelson Consultant Azane, Inc. Bethesda, MD, USA Missoula, MT, USA Cognizant Committees The chairperson of Refrigerant Committee also served as ex-officio members: Karim Amrane REF Committee AHRI Bethesda, MD, USA i © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. HISTORY of REVISION / REAFFIRMATION / WITHDRAWAL
    [Show full text]
  • Solar Thermal Energy
    22 Solar Thermal Energy Solar thermal energy is an application of solar energy that is very different from photovol- taics. In contrast to photovoltaics, where we used electrodynamics and solid state physics for explaining the underlying principles, solar thermal energy is mainly based on the laws of thermodynamics. In this chapter we give a brief introduction to that field. After intro- ducing some basics in Section 22.1, we will discuss Solar Thermal Heating in Section 22.2 and Concentrated Solar (electric) Power (CSP) in Section 22.3. 22.1 Solar thermal basics We start this section with the definition of heat, which sometimes also is called thermal energy . The molecules of a body with a temperature different from 0 K exhibit a disordered movement. The kinetic energy of this movement is called heat. The average of this kinetic energy is related linearly to the temperature of the body. 1 Usually, we denote heat with the symbol Q. As it is a form of energy, its unit is Joule (J). If two bodies with different temperatures are brought together, heat will flow from the hotter to the cooler body and as a result the cooler body will be heated. Dependent on its physical properties and temperature, this heat can be absorbed in the cooler body in two forms, sensible heat and latent heat. Sensible heat is that form of heat that results in changes in temperature. It is given as − Q = mC p(T2 T1), (22.1) where Q is the amount of heat that is absorbed by the body, m is its mass, Cp is its heat − capacity and (T2 T1) is the temperature difference.
    [Show full text]
  • Investigating Absorption Refrigerator Fires (Part I)
    Orion P. Keifer Peter D. Layson Charles A. Wensley Investigating Absorption Refrigerator Fires (Part I) ATLANTIC BEACH, FLORIDA—In today’s recreational vehicles (RV), the then expels it when perco- most common refrigerator uses absorption refrigeration technology, lated in the boiler. It is this primarily because this type of system can operate on multiple sources action of the water which of power, including propane when electrical power is unavailable. makes the ammonia flow. These refrigerators have been under intense scrutiny in recent years The hydrogen in the re- due to numerous reported fires, apparently starting in the area of the frigeration coil maintains absorption refrigerator. Both the Dometic Corporation and Norcold a positive pressure of ap- Incorporated, two manufacturers of RV refrigerators, have been re- proximately 300-375 PSI quired by the National Highway and Traffic Safety Administration (2.07-2.59 MPa) when (NHTSA) to recall certain models of refrigerators which have been not in operation and, due identified as capable of failing in a fire mode. In summary, the three to its low partial pressure, NHTSA recalls indicate a fatigue crack may develop in the boiler tube promotes the evaporation of the cooling unit which may release sufficient pressurized flammable of the liquid ammonia. It coolant solution into an area where an ignition source is present. The should be noted that unlike NHTSA Recall Campaign ID Numbers are 06E076000 for Dometic conventional refrigeration (926,877 affected units), and 02E019000 (28,144 affected units) and systems which extensively 02E045000 (8,419 affected units) for Norcold. use copper due to its high thermal conductivity, the Applications Engineering Group, Inc.
    [Show full text]
  • Solar Air-Conditioning and Refrigeration - Achievements and Challenges
    Solar air-conditioning and refrigeration - achievements and challenges Hans-Martin Henning Fraunhofer-Institut für Solare Energiesysteme ISE, Freiburg/Germany EuroSun 2010 September 28 – October 2, 2010 Graz - AUSTRIA © Fraunhofer ISE Outline Components and systems Achievements Solar thermal versus PV? Challenges and conclusion © Fraunhofer ISE Components and systems Achievements Solar thermal versus PV? Challenges and conclusion © Fraunhofer ISE Overall approach to energy efficient buildings Assure indoor comfort with a minimum energy demand 1. Reduction of energy demand Building envelope; ventilation 2. Use of heat sinks (sources) in Ground; outside air (T, x) the environment directly or indirectly; storage mass 3. Efficient conversion chains HVAC; combined heat, (minimize exergy losses) (cooling) & power (CH(C)P); networks; auxiliary energy 4. (Fractional) covering of the Solar thermal; PV; (biomass) remaining demand using renewable energies © Fraunhofer ISE Solar thermal cooling - basic principle Basic systems categories Closed cycles (chillers): chilled water Open sorption cycles: direct treatment of fresh air (temperature, humidity) © Fraunhofer ISE Open cycles – desiccant air handling units Solid sorption Liquid sorption Desiccant wheels Packed bed Coated heat exchangers Plate heat exchanger Silica gel or LiCl-matrix, future zeolite LiCl-solution: Thermochemical storage possible ECOS (Fraunhofer ISE) in TASK 38 © Fraunhofer ISE Closed cycles – water chillers or ice production Liquid sorption: Ammonia-water or Water-LiBr (single-effect or double-effect) Solid sorption: silica gel – water, zeolite-water Ejector systems Thermo-mechanical systems Turbo Expander/Compressor AC-Sun, Denmark in TASK 38 © Fraunhofer ISE System overview Driving Collector type System type temperature Low Open cycle: direct air treatment (60-90°C) Closed cycle: high temperature cooling system (e.g.
    [Show full text]
  • Empirical Modelling of Einstein Absorption Refrigeration System
    Journal of Advanced Research in Fluid Mechanics and Thermal Sciences 75, Issue 3 (2020) 54-62 Journal of Advanced Research in Fluid Mechanics and Thermal Sciences Journal homepage: www.akademiabaru.com/arfmts.html ISSN: 2289-7879 Empirical Modelling of Einstein Absorption Refrigeration Open Access System Keng Wai Chan1,*, Yi Leang Lim1 1 School of Mechanical Engineering, Engineering Campus, Universiti Sains Malaysia, 14300 Nibong Tebal, Penang, Malaysia ARTICLE INFO ABSTRACT Article history: A single pressure absorption refrigeration system was invented by Albert Einstein and Received 4 April 2020 Leo Szilard nearly ninety-year-old. The system is attractive as it has no mechanical Received in revised form 27 July 2020 moving parts and can be driven by heat alone. However, the related literature and Accepted 5 August 2020 work done on this refrigeration system is scarce. Previous researchers analysed the Available online 20 September 2020 refrigeration system theoretically, both the system pressure and component temperatures were fixed merely by assumption of ideal condition. These values somehow have never been verified by experimental result. In this paper, empirical models were proposed and developed to estimate the system pressure, the generator temperature and the partial pressure of butane in the evaporator. These values are important to predict the system operation and the evaporator temperature. The empirical models were verified by experimental results of five experimental settings where the power input to generator and bubble pump were varied. The error for the estimation of the system pressure, generator temperature and partial pressure of butane in evaporator are ranged 0.89-6.76%, 0.23-2.68% and 0.28-2.30%, respectively.
    [Show full text]
  • A Review on Solar Powered Refrigeration and the Various Cooling Thermal Energy Storage (CTES) Systems
    International Journal of Engineering Research & Technology (IJERT) ISSN: 2278-0181 Vol. 2 Issue 2, February- 2013 A review on Solar Powered Refrigeration and the Various Cooling Thermal Energy Storage (CTES) Systems 1*Abhishek Sinha and 2 S. R Karale rd 1* Student, III Semester, M.Tech.Heat Power Engineering, 2 Professor Mechanical Engineering Department, G.H Raisoni College of Engineering, Nagpur-440016, India Abstract In this paper, a review has been conducted on various types of methods which are available for utilizing solar energy for refrigeration purposes. Solar refrigeration methods such as Solar Electric Method, Solar Mechanical Method and Solar Thermal Methods have been discussed. In solar thermal methods, various methods like Desiccant Refrigeration, Absorption Refrigeration and Adsorption Refrigeration has been discussed. All the methods have been assesed economically and environmentally and their operating characteristics have been compared to establish the best possible method for solar refrigeration. Also, the various available technologies for Cooling Thermal Energy Storage (CTES) have been discussed in this paper. Methods like Chilled Water Storage (CWS) and Ice Thermal Storage (ITS) have been compared and their advantages and disadvantages have been IJERTdiscussed.IJERT The results of the review reveal Solar Electric Method as the most promising method for solar refrigeration over the other methods. As far as CTES systems are concerned, ITS has advantage over other methods based on storage volume capability, but it has a comparatively lower COP than other available techniques. Keywords: Solar powered refrigeration, Solar Electric Method, Solar Mechanical Method, Solar Thermal Method, CTES system, Chilled Water Storage (CWS) system, ice TES systems, etc.
    [Show full text]
  • Teaching Psychrometry to Undergraduates
    AC 2007-195: TEACHING PSYCHROMETRY TO UNDERGRADUATES Michael Maixner, U.S. Air Force Academy James Baughn, University of California-Davis Michael Rex Maixner graduated with distinction from the U. S. Naval Academy, and served as a commissioned officer in the USN for 25 years; his first 12 years were spent as a shipboard officer, while his remaining service was spent strictly in engineering assignments. He received his Ocean Engineer and SMME degrees from MIT, and his Ph.D. in mechanical engineering from the Naval Postgraduate School. He served as an Instructor at the Naval Postgraduate School and as a Professor of Engineering at Maine Maritime Academy; he is currently a member of the Department of Engineering Mechanics at the U.S. Air Force Academy. James W. Baughn is a graduate of the University of California, Berkeley (B.S.) and of Stanford University (M.S. and PhD) in Mechanical Engineering. He spent eight years in the Aerospace Industry and served as a faculty member at the University of California, Davis from 1973 until his retirement in 2006. He is a Fellow of the American Society of Mechanical Engineering, a recipient of the UCDavis Academic Senate Distinguished Teaching Award and the author of numerous publications. He recently completed an assignment to the USAF Academy in Colorado Springs as the Distinguished Visiting Professor of Aeronautics for the 2004-2005 and 2005-2006 academic years. Page 12.1369.1 Page © American Society for Engineering Education, 2007 Teaching Psychrometry to Undergraduates by Michael R. Maixner United States Air Force Academy and James W. Baughn University of California at Davis Abstract A mutli-faceted approach (lecture, spreadsheet and laboratory) used to teach introductory psychrometric concepts and processes is reviewed.
    [Show full text]
  • Thermodynamics of Interacting Magnetic Nanoparticles
    This is a repository copy of Thermodynamics of interacting magnetic nanoparticles. White Rose Research Online URL for this paper: https://eprints.whiterose.ac.uk/168248/ Version: Accepted Version Article: Torche, P., Munoz-Menendez, C., Serantes, D. et al. (6 more authors) (2020) Thermodynamics of interacting magnetic nanoparticles. Physical Review B. 224429. ISSN 2469-9969 https://doi.org/10.1103/PhysRevB.101.224429 Reuse Items deposited in White Rose Research Online are protected by copyright, with all rights reserved unless indicated otherwise. They may be downloaded and/or printed for private study, or other acts as permitted by national copyright laws. The publisher or other rights holders may allow further reproduction and re-use of the full text version. This is indicated by the licence information on the White Rose Research Online record for the item. Takedown If you consider content in White Rose Research Online to be in breach of UK law, please notify us by emailing [email protected] including the URL of the record and the reason for the withdrawal request. [email protected] https://eprints.whiterose.ac.uk/ Thermodynamics of interacting magnetic nanoparticles P. Torche1, C. Munoz-Menendez2, D. Serantes2, D. Baldomir2, K. L. Livesey3, O. Chubykalo-Fesenko4, S. Ruta5, R. Chantrell5, and O. Hovorka1∗ 1School of Engineering and Physical Sciences, University of Southampton, Southampton SO16 7QF, UK 2Instituto de Investigaci´ons Tecnol´oxicas and Departamento de F´ısica Aplicada, Universidade de Santiago de Compostela,
    [Show full text]
  • Understanding Psychrometrics, Third Edition It’S Really a Mine of Information
    Gatley The Comprehensive Guide to Psychrometrics Understanding Psychrometrics serves as a lifetime reference manual and basic refresher course for those who use psychrometrics on a recurring basis and provides a four- to six-hour psychrometrics learning module to students; air- conditioning designers; agricultural, food process, and industrial process engineers; Understanding Psychrometrics meteorologists and others. Understanding Psychrometrics Third Edition New in the Third Edition • Revised chapters for wet-bulb temperature and relative humidity and a revised Appendix V that includes a summary of ASHRAE Research Project RP-1485. • New constants for the universal gas constant based on CODATA and a revised molar mass of dry air to account for the increase of CO2 in Earth’s atmosphere. • New IAPWS models for the calculation of water properties above and below freezing. • New tables based on the ASHRAE RP-1485 real moist-air numerical model using the ASHRAE LibHuAirProp add-ins for Excel®, MATLAB®, Mathcad®, and EES®. Includes Access to Bonus Materials and Sample Software • PDF files of 13 ultra-high-pressure and 12 existing ASHRAE psychrometric charts plus three new 0ºC to 400ºC charts. • A limited demonstration version of the ASHRAE LibHuAirProp add-in that allows users to duplicate portions of the real moist-air psychrometric tables in the ASHRAE Handbook—Fundamentals for both standard sea level atmospheric pressure and pressures from 5 to 10,000 kPa. • The hw.exe program from the second edition, included to enable users to compare the 2009 ASHRAE numerical model real moist-air psychrometric properties with the 1983 ASHRAE-Hyland-Wexler properties. Praise for Understanding Psychrometrics, Third Edition It’s really a mine of information.
    [Show full text]
  • Quantized Refrigerator for an Atomic Cloud
    Quantized refrigerator for an atomic cloud Wolfgang Niedenzu1, Igor Mazets2,3, Gershon Kurizki4, and Fred Jendrzejewski5 1Institut für Theoretische Physik, Universität Innsbruck, Technikerstraße 21a, A-6020 Innsbruck, Austria 2Vienna Center for Quantum Science and Technology (VCQ), Atominstitut, TU Wien, 1020 Vienna, Austria 3Wolfgang Pauli Institute, c/o Fakultät für Mathematik, Universität Wien, 1090 Vienna, Austria 4Department of Chemical Physics, Weizmann Institute of Science, Rehovot 7610001, Israel 5Heidelberg University, Kirchhoff-Institut für Physik, Im Neuenheimer Feld 227, D-69120 Heidelberg, Germany June 24, 2019 We propose to implement a quantized ther- a) mal machine based on a mixture of two atomic species. One atomic species implements the working medium and the other implements two (cold and hot) baths. We show that such a setup can be employed for the refrigeration of a large bosonic cloud starting above and end- ing below the condensation threshold. We ana- lyze its operation in a regime conforming to the b) quantized Otto cycle and discuss the prospects for continuous-cycle operation, addressing the experimental as well as theoretical limitations. <latexit sha1_base64="xPORfqE4jiv0WYJsIrI5dlUB7fE=">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</latexit>Beyond
    [Show full text]